Adsorption measurements at 298K for N2,CO2, and CH4 on three different microporous adsorbents prepared in KH 142, are given in the excel file uploaded on canvas. (1) Fit all pure-component adsorption data to the following empirical adsorption isotherm (known as SIPS isotherm): q=q01+bp1bp1 Where q is the pure-component molar loading at pressure p. For each gas, the non-linear fit should produce the values of q0,b, and n. (2) Use the results of (1) and the Ideal Adsorbed Solution Theory as explained in class, to calculate binary adsorption isotherms for all possible binary mixtures in all 3 adsorbents. Component A (or 1 ) should be the strongest adsorbate. Assume yA=0.15 and consider a range of pressures from p=30 torr to p=760 torr. In the report, include plots of the selectivity and the molar loadings in terms of pressure. Adsorption measurements at 298K for N2,CO2, and CH4 on three different microporous adsorbents prepared in KH 142, are given in the excel file uploaded on canvas. (1) Fit all pure-component adsorption data to the following empirical adsorption isotherm (known as SIPS isotherm): q=q01+bp1bp1 Where q is the pure-component molar loading at pressure p. For each gas, the non-linear fit should produce the values of q0,b, and n. (2) Use the results of (1) and the Ideal Adsorbed Solution Theory as explained in class, to calculate binary adsorption isotherms for all possible binary mixtures in all 3 adsorbents. Component A (or 1 ) should be the strongest adsorbate. Assume yA=0.15 and consider a range of pressures from p=30 torr to p=760 torr. In the report, include plots of the selectivity and the molar loadings in terms of pressure